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INVENTION
Russian Federation Patent RU2173303
BIOMETANOVY HEAT
Name of the inventor: Viktor Tumchenok Ignatievich
The name of the patentee: Tumchenok Victor Ignatievich
Address for correspondence: 680035, Khabarovsk, ul. Cooper, 1, kv.66, V.I.Tumchenku
Starting date of the patent: 2000.01.14
The invention relates to a biological waste and agricultural processing wastes generation of methane as a fuel in a mixture with liquid lithium in the plasma state. The heat exchanger contains a collection of wastewater and waste, communication with the digester, consisting of cameras: an acidic, neutral, alkaline, methane fermentation, equipped with dispersants. The camera methane fermentation biogas and poslebrozhevoy fluid communication with the column enzymatic hydrolysis made of sections formed by transverse perforated baffles placed on them with the abrasive grain immobilization attachment. Section overflow pipe communicated and the upper of which communicates with methane teploelektrogeneratorom which is provided with a cylindrical chamber plasmolysis performed with paired tangential nozzles, docked with the grooves in the coating, such as graphite melt. Gutters have helical grooves, helices that are mirrored to each other and interfaced at the junction of the gutters. The invention improves the efficiency of the processing of agricultural waste and waste by increasing the production of methane.
DESCRIPTION OF THE INVENTION
The invention relates to a complex biological waste and agricultural run selhozstokov with the development of methane as a fuel in a mixture with liquid lithium in the plasma state to generate heat and power at the enterprises of agrarian and industrial complex to improve the environmental situation and reduce the cost of production of eggs, milk, meat and other agricultural products.
Known biometanovy recovery (BMU), which includes a collection of wastewater and waste, communication with the digester consisting of acidic cameras, neutral, alkaline, methane fermentation, equipped with dispersants, and the camera methane fermentation biogas and poslebrozhevoy fluid communication with the column enzymatic hydrolysis (EC) made of the sections formed by transverse perforated partitions (PPP) and placed on the RFP abrasive grain immobilization attachment (azine), and section reported on the flow of the fluid overflow tube, and the upper KF section methane communicated with teploelektrogeneratorom (patent RF N 2097421, cl. C 12 M 1/00, 1997), which is a drawback of high consumption of methane needs to teploelektrosnabzheniya combustion due to its doplazmennom condition that reduces the efficiency of operation BMU.
The purpose of the invention - efficiency - is achieved in that teploelektrogenerator (TEG) is provided with a cylindrical chamber plasmolysis performed with paired tangential nozzles, docked with the grooves in the coating, for example, from a melt of graphite, and the trough are provided with helical grooves, helices that are mirrored to each other and interfaced at the junction of the gutters.
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Rationale achieving invention will herein BMU operation. FIG. 1 schematically shows a general view BMU; FIG. 2 - A-A sectional view in FIG. 1; FIG. 3 - B-B sectional view in FIG. 2: FIG. 4 - view along arrow B in FIG. 2.
BMU includes a collection of 1 sewage and waste, communication with the digester 2, consisting of a camera 3 - sour, 4 - Neutral 5 - base, 6 - methane fermentation and the camera 6 methane fermentation biogas and poslebrozhevoy fluid communication with the CF 7 made of sections 8, formed by SPT 9 and placed on them azine 10, and section 8 for fluid flow reported overflow pipe 11, and the upper section 8 of the CF 7 communicates with teploelektrogeneratorom (TEG), equipped with a cylindrical chamber 12 plasmolysis made with conjugated tangential nozzles 13 and 14, docked with the grooves 15 and 16 in the cover 17, for example, graphite melt and troughs 15 and 16 are provided with helical grooves 18 and 19, the helical lines which are mirrored to each other and are associated at the junction 20 of gutters 15 and 16, which set acuminate electrodes 21 and 22 are connected to the voltage pulse generator 23 (GAI). Plasmolysis chamber 12 communicates with the firebox 24 and TEG with struevoy compressor 25 which in turn communicates with a compressor 26 struevoy methane collector 27 and the container 28 of liquid lithium. By firing axis 24 has pointed electrodes 29 and 30 communicated with a voltage pulse generator (SAI) 31 and concentric electrodes 29 and 30, the electrodes 32 and 33 are communicated with the load current collector 34. Camera axis 12 is placed low voltage arc the arc electrodes 35 36 and 37.
BMU WORKS AS FOLLOWS
Waste products of animal and poultry gidrosmyvom and gidrosplavom enter the collector 1, to which is added agricultural run to adjust the ratio between carbon and nitrogen to 20: 1, and agricultural run pulverized dispersing 38 to a particle size comparable to the size-utilizing microflora in the digester 2 (kislotogeny, acetogens , ... atsetogidrogeny methanogens) occurs with temperature control to ensure that temperature variations do not exceed one degree per day to avoid acidification of the substrate in each chamber. Job 38 addition of dispersants thermostat causes the destruction of gas bubbles around the substrate weighed against the generation of new generations of microflora occurring every 20-30 minutes, which destroys old cells while sparing effect on the young. Biogas is subjected to the exhaustion of carbon and hydrogen sulfide in the KF 7. Under the influence of the azine destroyed shell 10 with old cells release enzymes that decompose water into hydrogen and oxygen. The oxygen oxidizes the hydrogen sulfide to sulfur microcell and hydrogen to methane recovers carbon dioxide concentration, and increasing its output per unit volume of the substrate. Methane from the collection 27 in admixture with liquid lithium from the cylinder 28 struevoy compressor 26 is pumped into the chamber 12 plasmolysis. At speeds of about 100 m / s a mixture of tangential nozzles 13 and 14 in the trenches 15 and 16 passes into a plasma with an arc 35 from burning of the low voltage arc electrodes 36 and 37. The screw groove 18 and 19 match the jet 15 spouts 16 and 20 at the juncture of the pressure in the contact area increases to hundreds of thousands of atmospheres, leading to the convergence action radii nuclei to atomic forces and synthesis of helium. The pointed electrodes 21 and 22, 23 GAI initiate the plasma and report it to move the light velocity "spooling" with respect to the plasma arc 35. The plasma arc excess of pointed electrodes 35 and 21 and switches 22, SAI 23 24 TEG into the furnace and burned therein to form plasma of chilled with heat removal circuit (not shown). The pulses between the electrodes 29 and 30 of the SAI 31 is moved from the plasma chamber 12 to struevoy compressor 25 in a closed loop, after separation struevoy helium compressor 26. When moving forward current between the electrodes 29 and 30 of the SAI 31 in the electrodes 32 and 33 of the self-inductance of a current machineless production, during which time the load 34, and this current is equal in magnitude to the direct current from the SAI 31. Transfer of fuel in the chamber 12 to the combustion chamber 24 plasmolysis TEG into a plasma state and its burning at a temperature of 940-980 o C significantly reduces its consumption for heating needs and supply of agricultural enterprises. An indicator of calories for carbon-hydrogen fuel is an H: C, gasoline is equal to 2.2, for about 2 kerosene, coal is less than 1, and for methane is 4, ie, methane in calories is the preferred fuel for agriculture. When developing the conditions of enzymatic hydrolysis of methane in its output increased to 1.3-1.5 kg per 1 kg of the consumption of organic selhozstokov and waste.
A feature of the methane as fuel for the needs of heat and electrical energy is ecological cleanliness and safety for the environment, especially when operating in a closed cycle. Water after KF 7 returns to the needs and gidrosmyva gidrosplava that minimizes the consumption of fresh.
Recovery coating 17 from exposure to the plasma is carried out by implantation of material erosion pointed electrodes 21 and 22, which include tungsten and lanthanum hexaboride. As used azines 10 Circulite modified zeolite having a low density.
CLAIM
Biometanovy recovery, including a collection of wastewater and waste, communication with the digester, consisting of cameras: an acidic, neutral, alkaline, methane fermentation, equipped with dispersants, and the camera methane fermentation biogas and poslebrozhevoy fluid communication with the column enzymatic hydrolysis made of sections formed by transverse perforated septa and placed on the partitions abrasive grain immobilization attachment while section communicated downstream fluid overflow pipe and the upper section of the column enzymatic hydrolysis methane communicates with teploelektrogeneratorom, wherein teploelektrogenerator provided with a cylindrical chamber plasmolysis performed with paired tangential nozzles, docked with gutters in the coating, such as graphite from the melt, and the trough are provided with helical grooves, helices which are mirrored to each other and at the junction conjugate gutters.
print version
Publication date 05.01.2007gg
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